CA3036075A1 - Process for the production of a pgm-enriched alloy - Google Patents
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C19/00—Alloys based on nickel or cobalt
- C22C19/03—Alloys based on nickel or cobalt based on nickel
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- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/02—Obtaining noble metals by dry processes
- C22B11/021—Recovery of noble metals from waste materials
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
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- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
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- C22B11/00—Obtaining noble metals
- C22B11/02—Obtaining noble metals by dry processes
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- C22B11/00—Obtaining noble metals
- C22B11/02—Obtaining noble metals by dry processes
- C22B11/021—Recovery of noble metals from waste materials
- C22B11/025—Recovery of noble metals from waste materials from manufactured products, e.g. from printed circuit boards, from photographic films, paper, or baths
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- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/02—Obtaining noble metals by dry processes
- C22B11/021—Recovery of noble metals from waste materials
- C22B11/026—Recovery of noble metals from waste materials from spent catalysts
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- C—CHEMISTRY; METALLURGY
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- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
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- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/05—Refining by treating with gases, e.g. gas flushing also refining by means of a material generating gas in situ
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- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/10—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C1/00—Making non-ferrous alloys
- C22C1/02—Making non-ferrous alloys by melting
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- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C1/00—Making non-ferrous alloys
- C22C1/02—Making non-ferrous alloys by melting
- C22C1/023—Alloys based on nickel
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- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
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- C22C1/00—Making non-ferrous alloys
- C22C1/06—Making non-ferrous alloys with the use of special agents for refining or deoxidising
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- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C3/00—Removing material from alloys to produce alloys of different constitution separation of the constituents of alloys
- C22C3/005—Separation of the constituents of alloys
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- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C5/00—Alloys based on noble metals
- C22C5/04—Alloys based on a platinum group metal
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B14/00—Crucible or pot furnaces
- F27B14/08—Details peculiar to crucible or pot furnaces
- F27B14/14—Arrangements of heating devices
- F27B14/143—Heating of the crucible by convection of combustion gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/16—Introducing a fluid jet or current into the charge
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/16—Introducing a fluid jet or current into the charge
- F27D2003/168—Introducing a fluid jet or current into the charge through a lance
- F27D2003/169—Construction of the lance, e.g. lances for injecting particles
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
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Abstract
A process for the production of a PGM-enriched alloy comprising 0 to 60 wt.-% of iron and 20 to 99 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, the process comprising the steps of (1) providing a PGM collector alloy comprising 30 to 95 wt.-% of iron, less than 1 wt.-% of sulfur and 2 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, (2) providing a copper- and sulfur-free material capable of forming a slag-like composition when molten, wherein the molten slag-like composition comprises 40 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 60 wt.-% of silicon dioxide, (3) melting the PGM collector alloy and the material capable of forming a slag-like composition when molten in a weight ratio of 1 : 0.2 to 1 within a converter until a multi- or two-phase system of a lower high-density molten mass comprising the molten PGM collector alloy and one or more upper low-density molten masses comprising the molten slag-like composition has formed, (4) contacting an oxidizing gas comprising 0 to 80 vol.-% of inert gas and 20 to 100 vol.-% of oxygen with the lower high-density molten mass obtained in step (3) until it has been converted into a lower high-density molten mass of the PGM-enriched alloy, (5) separating an upper low-density molten slag formed in the course of step (4) from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density, (6) letting the molten masses separated from one another cool down and solidify, and (7) collecting the solidified PGM-enriched alloy.
Description
Process for the Production of a PGM-enriched alloy CROSS REFERENCE TO RELATED APPLICATIONS
100011 This application claims the benefit of U.S. Non-Provisional Application No.
15/355,971 filed November 18, 2016, the entire contents of which are incorporated by reference herein.
FILED OF THE INVENTION
100011 This application claims the benefit of U.S. Non-Provisional Application No.
15/355,971 filed November 18, 2016, the entire contents of which are incorporated by reference herein.
FILED OF THE INVENTION
[0002] The invention relates to a pyrometallurgical converting process for the production of a PGM-enriched alloy and to the PGM-enriched alloy itself.
[0003] The abbreviation "PGM" used herein means platinum group metal.
DESCRIPTION OF RELATED ART
DESCRIPTION OF RELATED ART
[0004] In general, the enrichment of PGMs by means of pyrometallurgical converting is well-known, see, for example, S.D. MCCULLOUGH, Pyrometallurgical iron removal from a PGM-containing alloy, Third International Platinum Conference Platinum in Transformation', The Southern African Institute of Mining and Metallurgy, 2008, pages 1-8.
DETAILED DESCRIPTION
DETAILED DESCRIPTION
[0005] The invention is a pyrometallurgical converting process improved in terms of yielding a PGM-enriched alloy having a considerable high PGM level and exhibiting a remarkably low PGM loss into slag formed as by-product of the pyrometallurgical converting process.
[0006] The process of the invention is a process for the production of a PGM-enriched alloy comprising 0 to 60 wt.-% (weight-%) of iron and 20 to 99 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium.
The process comprises the steps:
(1) providing a PGM collector alloy comprising 30 to 95 wt.-% of iron, less than 1 wt.-%
of sulfur and 2 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, (2) providing a copper- and sulfur-free material capable of forming a slag-like composition when molten, wherein the molten slag-like composition comprises 40 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 60 wt.-% of silicon dioxide, (3) melting the PGM collector alloy and the material capable of forming a slag-like composition when molten in a weight ratio of 1 : 0.2 to 1 within a converter until a multi-or two-phase system of a lower high-density molten mass comprising the molten PGM
collector alloy and one or more upper low-density molten masses comprising the molten slag-like composition has formed, (4) contacting an oxidizing gas comprising 0 to 80 vol.-% (volume-%) of inert gas and 20 to 100 vol.-% of oxygen with the lower high-density molten mass obtained in step (3) until it has been converted into a lower high-density molten mass of the PGM-enriched alloy (i.e. a lower high-density molten mass of the composition of the PGM-enriched alloy), (5) separating an upper low-density molten slag formed in the course of step (4) from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density, (6) letting the molten masses separated from one another cool down and solidify, and
The process comprises the steps:
(1) providing a PGM collector alloy comprising 30 to 95 wt.-% of iron, less than 1 wt.-%
of sulfur and 2 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, (2) providing a copper- and sulfur-free material capable of forming a slag-like composition when molten, wherein the molten slag-like composition comprises 40 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 60 wt.-% of silicon dioxide, (3) melting the PGM collector alloy and the material capable of forming a slag-like composition when molten in a weight ratio of 1 : 0.2 to 1 within a converter until a multi-or two-phase system of a lower high-density molten mass comprising the molten PGM
collector alloy and one or more upper low-density molten masses comprising the molten slag-like composition has formed, (4) contacting an oxidizing gas comprising 0 to 80 vol.-% (volume-%) of inert gas and 20 to 100 vol.-% of oxygen with the lower high-density molten mass obtained in step (3) until it has been converted into a lower high-density molten mass of the PGM-enriched alloy (i.e. a lower high-density molten mass of the composition of the PGM-enriched alloy), (5) separating an upper low-density molten slag formed in the course of step (4) from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density, (6) letting the molten masses separated from one another cool down and solidify, and
(7) collecting the solidified PGM-enriched alloy.
[0007] "0 wt.-%" or "0 vol.-%" appears several times in the description and the claims; it means that the respective component is not present or, if present, it is at best present in a proportion of no more than at a technically inevitable impurity level.
[0007] "0 wt.-%" or "0 vol.-%" appears several times in the description and the claims; it means that the respective component is not present or, if present, it is at best present in a proportion of no more than at a technically inevitable impurity level.
[0008] The process of the invention is a process for the production of a PGM-enriched alloy comprising 0 to 60 wt.-% of iron and 20 to 99 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium. It is preferred that the PGM-enriched alloy produced by the process of the invention comprises 0 to 45 wt.-%
of iron and 30 to 99 wt.-% of one or more of said PGMs, in particular 0 to 20 wt.-% of iron and 40 to 90 wt.-% of one or more of said PGMs. The PGM-enriched alloy made by the process of the invention may also comprise 0 to 60 wt.-% of nickel and 0 to 5 wt.-%
of copper. Examples of other elements (elements other than iron, nickel, copper, platinum, palladium and rhodium) which may be comprised by the PGM-enriched alloy made by the process of the invention include, in particular, silver, gold, aluminum, calcium and silicon. The PGM-enriched alloy made by the process of the invention may comprise one or more of said other elements in a total proportion of up to 10 wt.-%.
Hence, the PGM-enriched alloy made by the process of the invention may comprise or consist of:
0 to 60 wt.-%, preferably 0 to 45 wt.-%, in particular 0 to 20 wt.-% of iron, 20 to 99 wt.-%, preferably 30 to 99 wt.-%, in particular 40 to 90 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, 0 to 60 wt.-% of nickel, 0 to 5 wt.-% of copper, and 0 to 10 wt.-%, preferably 0 to 6 wt.-%, in particular 0 to 3 wt.-% of one or more other elements, in particular, one or more other elements selected from the group consisting of silver, gold, aluminum, calcium and silicon.
of iron and 30 to 99 wt.-% of one or more of said PGMs, in particular 0 to 20 wt.-% of iron and 40 to 90 wt.-% of one or more of said PGMs. The PGM-enriched alloy made by the process of the invention may also comprise 0 to 60 wt.-% of nickel and 0 to 5 wt.-%
of copper. Examples of other elements (elements other than iron, nickel, copper, platinum, palladium and rhodium) which may be comprised by the PGM-enriched alloy made by the process of the invention include, in particular, silver, gold, aluminum, calcium and silicon. The PGM-enriched alloy made by the process of the invention may comprise one or more of said other elements in a total proportion of up to 10 wt.-%.
Hence, the PGM-enriched alloy made by the process of the invention may comprise or consist of:
0 to 60 wt.-%, preferably 0 to 45 wt.-%, in particular 0 to 20 wt.-% of iron, 20 to 99 wt.-%, preferably 30 to 99 wt.-%, in particular 40 to 90 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, 0 to 60 wt.-% of nickel, 0 to 5 wt.-% of copper, and 0 to 10 wt.-%, preferably 0 to 6 wt.-%, in particular 0 to 3 wt.-% of one or more other elements, in particular, one or more other elements selected from the group consisting of silver, gold, aluminum, calcium and silicon.
[0009] In an embodiment, the PGM-enriched alloy made by the process of the invention comprises or consists of 0 to 20 wt.-% of iron, 40 to 90 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, 0 to 60 wt.-% of nickel, 0 to 5 wt.-% of copper and 0 to 3 wt.-% of one or more other elements, in particular, one or more other elements selected from the group consisting of silver, gold, aluminum, calcium and silicon.
[0010] In step (1) of the process of the invention a PGM collector alloy is provided.
[0011] PGM collector alloys are well-known to the person skilled in the art;
they may typically be formed during pyrometallurgic recycling of appropriate PGM
containing waste material like, for example, PGM containing waste catalysts, for example, used automotive exhaust catalysts. In the course of such pyrometallurgic recycling the PGMs are separated by smelting the PGM containing waste material, for example, ceramic supports having a PGM containing washcoat (like used automotive exhaust catalysts) together with a collector metal like, for example, iron in an oven, a so-called smelter.
The PGMs form a PGM collector alloy with the collector metal, which is separated from slag formed as by-product during smelting.
they may typically be formed during pyrometallurgic recycling of appropriate PGM
containing waste material like, for example, PGM containing waste catalysts, for example, used automotive exhaust catalysts. In the course of such pyrometallurgic recycling the PGMs are separated by smelting the PGM containing waste material, for example, ceramic supports having a PGM containing washcoat (like used automotive exhaust catalysts) together with a collector metal like, for example, iron in an oven, a so-called smelter.
The PGMs form a PGM collector alloy with the collector metal, which is separated from slag formed as by-product during smelting.
[0012] The PGM collector alloy provided in step (1) comprises 30 to 95 wt.-%
of iron;
less than 1 wt.-% or, in particular, even 0 wt.-% of sulfur; and 2 to 15 wt.-%
of one or more PGMs selected from the group consisting of platinum, palladium and rhodium.
of iron;
less than 1 wt.-% or, in particular, even 0 wt.-% of sulfur; and 2 to 15 wt.-%
of one or more PGMs selected from the group consisting of platinum, palladium and rhodium.
[0013] In an embodiment, the PGM collector alloy may comprise 40 to 70 wt.-%
of iron;
0 to 20 wt.-% of nickel; less than 1 wt.-% or, in particular, even 0 wt.-% of sulfur; and 5 to 15 wt.-% of one or more of said PGMs. It is preferred that the PGM
collector alloy comprises no more than 4 wt.-%, in particular 1 wt.-% of copper. Examples of other elements (elements other than iron, nickel, sulfur, copper, platinum, palladium and rhodium) which may be comprised by the PGM collector alloy include silver, gold, aluminum, calcium, silicon, phosphorus, titanium, chromium, manganese, molybdenum and vanadium. The PGM collector alloy may comprise one or more of said other elements in a total proportion of up to 30 wt.-%. Hence, the PGM collector alloy may comprise or consist of:
30 to 95 wt.-%, in particular 40 to 70 wt.-% of iron, 0 to 20 wt.-%, in particular 0 to 15 wt.-% of nickel, 2 to 15 wt.-%, in particular 5 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, less than 1 wt.-%, in particular 0 wt.-% of sulfur, 0 to 4 wt.-%, in particular 0 to 1 wt.-% of copper, and 0 to 30 wt.-%, in particular 0 to 20 wt.-% of one or more other elements, in particular, one or more other elements selected from the group consisting of silver, gold, aluminum, calcium, silicon, phosphorus, titanium, chromium, manganese, molybdenum and vanadium.
of iron;
0 to 20 wt.-% of nickel; less than 1 wt.-% or, in particular, even 0 wt.-% of sulfur; and 5 to 15 wt.-% of one or more of said PGMs. It is preferred that the PGM
collector alloy comprises no more than 4 wt.-%, in particular 1 wt.-% of copper. Examples of other elements (elements other than iron, nickel, sulfur, copper, platinum, palladium and rhodium) which may be comprised by the PGM collector alloy include silver, gold, aluminum, calcium, silicon, phosphorus, titanium, chromium, manganese, molybdenum and vanadium. The PGM collector alloy may comprise one or more of said other elements in a total proportion of up to 30 wt.-%. Hence, the PGM collector alloy may comprise or consist of:
30 to 95 wt.-%, in particular 40 to 70 wt.-% of iron, 0 to 20 wt.-%, in particular 0 to 15 wt.-% of nickel, 2 to 15 wt.-%, in particular 5 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, less than 1 wt.-%, in particular 0 wt.-% of sulfur, 0 to 4 wt.-%, in particular 0 to 1 wt.-% of copper, and 0 to 30 wt.-%, in particular 0 to 20 wt.-% of one or more other elements, in particular, one or more other elements selected from the group consisting of silver, gold, aluminum, calcium, silicon, phosphorus, titanium, chromium, manganese, molybdenum and vanadium.
[0014] If the PGM collector alloy comprises silicon, there may be two variants. In a first variant the silicon content of the PGM collector alloy may be in the range of 0 to 4 wt.-%, in a second variant it may be in the range of > 4 to 15 wt.-%.
[0015] In an embodiment, the PGM collector alloy comprises or consists of 40 to 70 wt.-% of iron, 0 to 15 wt.-% of nickel, 5 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, 0 to < 1 wt.-% of sulfur, 0 to 1 wt.-% of copper, 0 to 20 wt.-% of one or more other elements, in particular, one or more other elements selected from the group consisting of silver, gold, aluminum, calcium, silicon, phosphorus, titanium, chromium, manganese, molybdenum and vanadium.
[0016] In step (2) of the process of the invention a copper- and sulfur-free material capable of forming a slag-like composition when molten (hereinafter also called "material capable of forming a slag-like composition when molten" for short) is provided.
[0017] The term "copper- and sulfur-free" used herein in the context of step (2) of the process of the invention means that the material capable of forming a slag-like composition when molten may comprise copper and sulfur, each of both however in a proportion of no more than at a technically inevitable impurity level of, for example, less than 1000 wt.-ppm.
[0018] The term "material capable of forming a slag-like composition when molten" used herein shall illustrate that the molten material looks and behaves like a slag. It shall at the same time express that it is not to be confused with the slag formed as by-product of the process of the invention, i.e. the slag obtained after conclusion of step (4).
Moreover, the material capable of forming a slag-like composition when molten is not necessarily identical in composition with the one or more upper low-density molten masses formed in step (3), although it forms at least a predominant part of the latter.
Moreover, the material capable of forming a slag-like composition when molten is not necessarily identical in composition with the one or more upper low-density molten masses formed in step (3), although it forms at least a predominant part of the latter.
[0019] The material capable of forming a slag-like composition when molten has a composition such that the molten slag-like composition comprises or consists of:
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, to 60 wt.-% of silicon dioxide, 0 to 20 wt.-%, in particular 0 wt.-% of iron oxide (in particular FeO), 0 to 20 wt.-%, in particular 0 to 10 wt.-% of sodium oxide, 0 to 20 wt.-%, in particular 0 to 10 wt.-% of boron oxide, and 0 to 2 wt.-%, in particular 0 wt.-% of aluminum oxide.
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, to 60 wt.-% of silicon dioxide, 0 to 20 wt.-%, in particular 0 wt.-% of iron oxide (in particular FeO), 0 to 20 wt.-%, in particular 0 to 10 wt.-% of sodium oxide, 0 to 20 wt.-%, in particular 0 to 10 wt.-% of boron oxide, and 0 to 2 wt.-%, in particular 0 wt.-% of aluminum oxide.
[0020] If the silicon content of the PGM collector alloy provided in step (1) is in the range of 0 to 4 wt.-%, it is expedient that the material capable of forming a slag-like composition when molten has a composition such that the molten slag-like composition comprises or consists of:
40 to 60 wt.-% of magnesium oxide and/or calcium oxide, 40 to 60 wt.-% of silicon dioxide, 0 to 20 wt.-%, in particular 0 wt.-% of iron oxide (in particular FeO), 0 to 20 wt.-%, in particular 0 to 10 wt.-% of sodium oxide, 0 to 20 wt.-%, in particular 0 to 10 wt.-% of boron oxide, and 0 to 2 wt.-%, in particular 0 wt.-% of aluminum oxide.
40 to 60 wt.-% of magnesium oxide and/or calcium oxide, 40 to 60 wt.-% of silicon dioxide, 0 to 20 wt.-%, in particular 0 wt.-% of iron oxide (in particular FeO), 0 to 20 wt.-%, in particular 0 to 10 wt.-% of sodium oxide, 0 to 20 wt.-%, in particular 0 to 10 wt.-% of boron oxide, and 0 to 2 wt.-%, in particular 0 wt.-% of aluminum oxide.
[0021] If the silicon content of the PGM collector alloy provided in step (1) is in the range of > 4 to 15 wt.-%, it is expedient that the material capable of forming a slag-like composition when molten has a composition such that the molten slag-like composition comprises or consists of:
60 to 90 wt.-% of magnesium oxide and/or calcium oxide, 10 to 40 wt.-% of silicon dioxide, 0 to 20 wt.-%, in particular 0 wt.-% of iron oxide (in particular FeO), 0 to 20 wt.-%, in particular 0 to 10 wt.-% of sodium oxide, 0 to 20 wt.-%, in particular 0 to 10 wt.-% of boron oxide, and 0 to 2 wt.-%, in particular 0 wt.-% of aluminum oxide.
60 to 90 wt.-% of magnesium oxide and/or calcium oxide, 10 to 40 wt.-% of silicon dioxide, 0 to 20 wt.-%, in particular 0 wt.-% of iron oxide (in particular FeO), 0 to 20 wt.-%, in particular 0 to 10 wt.-% of sodium oxide, 0 to 20 wt.-%, in particular 0 to 10 wt.-% of boron oxide, and 0 to 2 wt.-%, in particular 0 wt.-% of aluminum oxide.
[0022] In an embodiment, and apart from said wt.-% proportions of silicon dioxide and magnesium oxide and/or calcium oxide, the material capable of forming a slag-like composition when molten has a composition such that the molten slag-like composition comprises no iron oxide, 0 to 10 wt.-% of sodium oxide, 0 to 10 wt.-% of boron oxide and no aluminum oxide.
[0023] The material capable of forming a slag-like composition when molten and, as a consequence thereof, also the molten slag-like composition itself does not comprise PGMs with the exception of technically inevitable impurities. However, if the latter is present its proportion should be low; preferably such proportion does not exceed, for example, 10 wt.-ppm in the material capable of forming a slag-like composition when molten.
[0024] The material capable of forming a slag-like composition when molten is a combination of substances and may comprise the aforementioned oxides or only said oxides, however, this is not necessarily the case. It may instead or additionally comprise compounds capable of forming such oxides or oxide compositions when heated during formation of the one or more upper low-density molten masses. To name just a few examples of such type of compounds: carbonates are examples of compounds which may split off carbon dioxide and form the corresponding oxides when heated and melted during formation of the one or more upper low-density molten masses;
silicates are examples of compounds which may form the corresponding oxides and silicon dioxide when heated and melted during formation of the one or more upper low-density molten masses; borates are examples of compounds which may form the corresponding oxides and boron oxide when heated and melted during formation of the one or more upper low-density molten masses.
silicates are examples of compounds which may form the corresponding oxides and silicon dioxide when heated and melted during formation of the one or more upper low-density molten masses; borates are examples of compounds which may form the corresponding oxides and boron oxide when heated and melted during formation of the one or more upper low-density molten masses.
[0025] In step (3) of the process of the invention the PGM collector alloy and the material capable of forming a slag-like composition when molten are melted in a weight ratio of 1 : 0.2 to 1, preferably 1 : 0.2 to 0.8, even more preferably 1 : 0.2 to 0.6 within a converter until a multi-phase system of a lower high-density molten mass comprising the molten PGM collector alloy and two or more upper low-density molten masses for example, 1200 to 1800 C, preferably 1500 to 1700 C. Such heating may be performed by various means either alone or in combination, i.e. for example plasma heating, indirect electrical heating, arc heating, inductive heating, indirect heating with burners, direct heating with one or more gas burners from the above and any combination of said heating methods. Direct heating with gas burners capable of producing said high temperatures is a preferred method. Examples of useful gas burners include gas burners run with hydrogen or a hydrocarbon-based fuel gas and oxygen or nitrous oxide as oxidant.
[0029] After conclusion of step (3), i.e. once the multi- or two-phase system has formed, step (4) of the process of the invention is performed. In step (4) an oxidizing gas comprising or consisting of 0 to 80 vol.-% of inert gas and 20 to 100 vol.-%
of oxygen, preferably 0 to 50 vol.-% of inert gas and 50 to 100 vol.-% of oxygen, in particular 0 vol.-% inert gas and 100 vol.-% of oxygen (i.e. oxygen gas) is contacted with the lower high-density molten mass obtained in step (3) until the latter has been converted into a lower high-density molten mass of the PGM-enriched alloy, i.e. the PGM-enriched alloy, has formed. Any gas inert towards the lower high-density molten mass can be taken as the inert gas, in particular argon and/or nitrogen. In preferred embodiments, contact between the oxygen or oxygen containing oxidizing gas and the lower high-density molten mass can be made by passing or bubbling the gas through the lower high-density molten mass from the bottom of the converter and/or by means of a gas lance the exhaust of which being immersed into the lower high-density molten mass.
The duration of the contact with the oxidizing gas or, in other words, the amount of oxidizing gas employed depends on when the PGM-enriched alloy of the desired composition has formed. In still other words, the contact with the oxidizing gas is maintained for such period of time, until a PGM-enriched alloy with a desired composition according to any of the afore disclosed embodiments has formed; this will typically take 1 to 5 hours or 2 to 4 hours, for example. The development of the composition of the lower high-density molten mass during performance of step (4) until the PGM-enriched alloy of the desired composition has formed, can be tracked by standard analytical techniques, for example, XRF (X-ray fluorescence) analysis. As by-product an upper low-density molten slag is formed in the course of step (4).
[0030] The contact with the oxidizing gas leads to an exothermic oxidation reaction in the course of which nonprecious elements or metals are converted into oxides and absorbed by the one or more upper low-density molten masses. The oxidation process of step (4) results in depletion of elements or metals other than the PGMs, in particular in depletion of iron and, if present, other nonprecious elements or metals within the lower high-density molten mass or, if taking the reverse view, in PGM
enrichment within the lower high-density molten mass.
[0031] After conclusion of step (4), i.e. once the PGM-enriched alloy of the desired composition has formed, step (5) of the process of the invention is performed.
In said step (5) the upper low-density molten slag formed in step (4) is separated from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density. To this end, the content of the converter is carefully poured out making use of the well-known decantation principle. Once the upper low-density molten slag is decanted the lower high-density molten mass of the PGM-enriched alloy is poured into suitable containers.
[0032] Steps (3) to (5) of the process of the invention constitute a sequence of steps, in particular in direct succession. This needs to be understood in such sense that no further steps or at least no further fundamental steps are required or performed between or during said steps (3) to (5). Examples of optional non-fundamental steps are (i) the removal of part of upper low-density molten mass in the course of step (4) or (ii) addition of PGM collector alloy and/or material capable of forming a slag-like composition when molten in the course of step (4).
[0033] After conclusion of step (5) subsequent step (6) is performed, in which the separated molten masses are allowed to cool down and solidify.
[0034] After solidification the solidified PGM-enriched alloy is collected in step (7). It may then be subject to further conventional refinement, for example, electrometallurgical and/or hydrometallurgical refinement in order to finally obtain the individual PGMs either as metal or as PGM compound or as a solution of the latter.
[0035] It is the advantage of the process of the invention that the PGM-enriched alloy collected in step (7) is distinguished by a relatively high PGM content. This relatively high PGM content means less effort and less consumption of chemicals with a view to said further refinement processes. It is a further remarkable advantage of the process of the invention that the slag formed as by-product during step (4) comprises a very low PGM content of less than 50 wt.-ppm. It is not finally understood why, but it is believed that the 1 : 0.2 to 1 or 1 : 0.2 to 0.8 or 1 : 0.2 to 0.6 weight ratio combination of the specifically composed PGM collector alloy provided in step (1) and the specifically composed material capable of forming a slag-like composition when molten provided in step (2) is key in particular with regard to the remarkably low loss of PGMs into the slag formed as by-product during step (4) of the process of the invention.
[0036] The invention comprises the following embodiments:
[0037] 1. A process for the production of a PGM-enriched alloy comprising 0 to 60 wt.-%
of iron and 20 to 99 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, the process comprising the steps:
(1) providing a PGM collector alloy comprising 30 to 95 wt.-% of iron, less than 1 wt.-%
of sulfur and 2 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, (2) providing a copper- and sulfur-free material capable of forming a slag-like composition when molten, wherein the molten slag-like composition comprises 40 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 60 wt.-% of silicon dioxide, (3) melting the PGM collector alloy and the material capable of forming a slag-like composition when molten in a weight ratio of 1 : 0.2 to 1 within a converter until a multi-or two-phase system of a lower high-density molten mass comprising the molten PGM
collector alloy and one or more upper low-density molten masses comprising the molten slag-like composition has formed, (4) contacting an oxidizing gas comprising 0 to 80 vol.-% of inert gas and 20 to 100 vol.-% of oxygen with the lower high-density molten mass obtained in step (3) until it has been converted into a lower high-density molten mass of the PGM-enriched alloy, (5) separating an upper low-density molten slag formed in the course of step (4) from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density, (6) letting the molten masses separated from one another cool down and solidify, and (7) collecting the solidified PGM-enriched alloy.
[0038] 2. The process of embodiment 1, wherein the PGM-enriched alloy comprises or consists of 0 to 45 wt.-% of iron and 30 to 99 wt.-% of the one or more PGMs, 0 to 60 wt.-% of nickel, 0 to 5 wt.-% of copper, and 0 to 10 wt.-% of one or more other elements.
[0039] 3. The process of embodiment 1, wherein the PGM-enriched alloy comprises or consists of 0 to 20 wt.-% of iron, 40 to 90 wt.-% of the one or more PGMs, 0 to 60 wt.-%
of nickel, 0 to 5 wt.-% of copper and 0 to 3 wt.-% of the one or more other elements.
[0040] 4. The process of any one of the preceding embodiments, wherein the PGM
collector alloy provided in step (1) comprises 40 to 70 wt.-% of iron, 0 to 20 wt.-% of nickel, less than 1 wt.-% of sulfur and 5 to 15 wt.-% of the one or more PGMs.
[0041] 5. The process of any one of the preceding embodiments, wherein the PGM
collector alloy comprises no more than 4 wt.-% of copper.
[0042] 6. The process of any one of embodiments 1 to 3, wherein the PGM
collector alloy comprises or consists of:
30 to 95 wt.-% of iron, 0 to 20 wt.-% of nickel, 0 to < 1 wt.-% of sulfur, 2 to 15 wt.-% of the one or more PGMs, 0 to 4 wt.-% of copper, and 0 to 30 wt.-% of one or more other elements.
[0043] 7. The process of any one of embodiments 1 to 3, wherein the PGM
collector alloy comprises or consists of:
40 to 70 wt.-% of iron, 0 to 15 wt.-% of nickel, 0 to < 1 wt.-% of sulfur, to 15 wt.-% of the one or more PGMs, 0 to 1 wt.-% of copper, and 0 to 20 wt.-% of one or more other elements.
[0044] 8. The process of any one of the preceding embodiments, wherein the molten slag-like composition comprises or consists of:
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, to 60 wt.-% of silicon dioxide, 0 to 20 wt.-% of iron oxide, 0 to 20 wt.-% of sodium oxide, 0 to 20 wt.-% of boron oxide, and 0 to 2 wt.-% of aluminum oxide.
[0045] 9. The process of any one of embodiments 1 to 7, wherein the molten slag-like composition comprises or consists of:
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, 10 to 60 wt.-% of silicon dioxide, 0 wt.-% of iron oxide, 0 to 10 wt.-% of sodium oxide, 0 to 10 wt.-% of boron oxide, and 0 wt.-% of aluminum oxide.
[0046] 10. The process of any one of the preceding embodiments, wherein the PGM
collector alloy comprises 0 to 4 wt.-% of silicon and wherein the molten slag-like composition comprises 40 to 60 wt.-% of magnesium oxide and/or calcium oxide and 40 to 60 wt.-% of silicon dioxide.
[0047] 11. The process of any one of embodiments 1 to 9, wherein the PGM
collector alloy comprises > 4 to 15 wt.-% of silicon and wherein the molten slag-like composition comprises 60 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 40 wt.-%
of silicon dioxide.
[0048] 12. The process of any one of the preceding embodiments, wherein the PGM
collector alloy and the material capable of forming a slag-like composition when molten are melted in a weight ratio of 1 : 0.2 to 0.8 or 1 : 0.2 to 0.6.
[0049] 13. The process of any one of the preceding embodiments, wherein the temperature of the converter contents is raised to 1200 to 1800 C.
[0050] 14. The process of any one of the preceding embodiments, wherein the contact between the oxidizing gas and the lower high-density molten mass is made by passing or bubbling the gas through the lower high-density molten mass from the bottom of the converter and/or by means of a gas lance the exhaust of which being immersed into the lower high-density molten mass.
[0051] 15. The process of any one of the preceding embodiments, wherein the contact with the oxidizing gas takes 1 to 5 hours.
Examples Example 1 [0052] A premix of 500 kg of a PGM collector alloy comprising 47 wt.-% of iron, 14.1 wt.-% of nickel, 8.1 wt.-% of silicon, 4.6 wt.-% of palladium, 3.2 wt.-% of chromium, 2.5 wt.-% of titanium, 2.2 wt.-% of platinum, 1.8 wt.-% of manganese, 0.6 wt.-% of rhodium and 0.9 wt.-% of copper, 123 kg of calcium oxide, 75 kg of silicon dioxide, 15 kg of sodium carbonate and 15 kg of borax was portionwise introduced into an already 1500 C
hot cylindrical natural gas-heated furnace and further heated to 1700 C.
[0053] After a melting time of 10 hours a two-phase system of a lower high-density molten mass comprising the PGM collector alloy and an upper low-density molten mass comprising a slag-like composition was formed. Oxygen was introduced into the lower high-density molten mass via a ceramic pipe with an oxygen flow of 900 I/min.
After 2.5 hours the oxygen introduction was stopped. The upper low-density molten mass was poured into cast iron slag pots in order to cool down and solidify. The lower high-density molten mass was then poured into graphite molds in order to cool down and solidify.
After solidification and cooling down to ambient temperature both materials were analyzed by XRF.
Examples 2 and 3 [0054] Example 1 was repeated with the difference that the oxygen introduction took 2.75 hours (Example 2) or 3 hours (Example 3).
[0055] The results of the XRF analysis are compiled in Tables 1 and 2. All values are in wt.-%, except the values for the PGM content in the slag which are in wt.-ppm:
Element Example 1 Example 2 Example 3 Fe 29 35 40 Ni 1 1 1 Total PGM 49 47 44 Table 1: Composition of the solidified upper low-density mass (slag) Element Example 1 Example 2 Example 3 Fe 20 18 13 Ni 50 51 51 Table 2: Composition of the solidified lower high-density mass (PGM enriched alloy)
[0029] After conclusion of step (3), i.e. once the multi- or two-phase system has formed, step (4) of the process of the invention is performed. In step (4) an oxidizing gas comprising or consisting of 0 to 80 vol.-% of inert gas and 20 to 100 vol.-%
of oxygen, preferably 0 to 50 vol.-% of inert gas and 50 to 100 vol.-% of oxygen, in particular 0 vol.-% inert gas and 100 vol.-% of oxygen (i.e. oxygen gas) is contacted with the lower high-density molten mass obtained in step (3) until the latter has been converted into a lower high-density molten mass of the PGM-enriched alloy, i.e. the PGM-enriched alloy, has formed. Any gas inert towards the lower high-density molten mass can be taken as the inert gas, in particular argon and/or nitrogen. In preferred embodiments, contact between the oxygen or oxygen containing oxidizing gas and the lower high-density molten mass can be made by passing or bubbling the gas through the lower high-density molten mass from the bottom of the converter and/or by means of a gas lance the exhaust of which being immersed into the lower high-density molten mass.
The duration of the contact with the oxidizing gas or, in other words, the amount of oxidizing gas employed depends on when the PGM-enriched alloy of the desired composition has formed. In still other words, the contact with the oxidizing gas is maintained for such period of time, until a PGM-enriched alloy with a desired composition according to any of the afore disclosed embodiments has formed; this will typically take 1 to 5 hours or 2 to 4 hours, for example. The development of the composition of the lower high-density molten mass during performance of step (4) until the PGM-enriched alloy of the desired composition has formed, can be tracked by standard analytical techniques, for example, XRF (X-ray fluorescence) analysis. As by-product an upper low-density molten slag is formed in the course of step (4).
[0030] The contact with the oxidizing gas leads to an exothermic oxidation reaction in the course of which nonprecious elements or metals are converted into oxides and absorbed by the one or more upper low-density molten masses. The oxidation process of step (4) results in depletion of elements or metals other than the PGMs, in particular in depletion of iron and, if present, other nonprecious elements or metals within the lower high-density molten mass or, if taking the reverse view, in PGM
enrichment within the lower high-density molten mass.
[0031] After conclusion of step (4), i.e. once the PGM-enriched alloy of the desired composition has formed, step (5) of the process of the invention is performed.
In said step (5) the upper low-density molten slag formed in step (4) is separated from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density. To this end, the content of the converter is carefully poured out making use of the well-known decantation principle. Once the upper low-density molten slag is decanted the lower high-density molten mass of the PGM-enriched alloy is poured into suitable containers.
[0032] Steps (3) to (5) of the process of the invention constitute a sequence of steps, in particular in direct succession. This needs to be understood in such sense that no further steps or at least no further fundamental steps are required or performed between or during said steps (3) to (5). Examples of optional non-fundamental steps are (i) the removal of part of upper low-density molten mass in the course of step (4) or (ii) addition of PGM collector alloy and/or material capable of forming a slag-like composition when molten in the course of step (4).
[0033] After conclusion of step (5) subsequent step (6) is performed, in which the separated molten masses are allowed to cool down and solidify.
[0034] After solidification the solidified PGM-enriched alloy is collected in step (7). It may then be subject to further conventional refinement, for example, electrometallurgical and/or hydrometallurgical refinement in order to finally obtain the individual PGMs either as metal or as PGM compound or as a solution of the latter.
[0035] It is the advantage of the process of the invention that the PGM-enriched alloy collected in step (7) is distinguished by a relatively high PGM content. This relatively high PGM content means less effort and less consumption of chemicals with a view to said further refinement processes. It is a further remarkable advantage of the process of the invention that the slag formed as by-product during step (4) comprises a very low PGM content of less than 50 wt.-ppm. It is not finally understood why, but it is believed that the 1 : 0.2 to 1 or 1 : 0.2 to 0.8 or 1 : 0.2 to 0.6 weight ratio combination of the specifically composed PGM collector alloy provided in step (1) and the specifically composed material capable of forming a slag-like composition when molten provided in step (2) is key in particular with regard to the remarkably low loss of PGMs into the slag formed as by-product during step (4) of the process of the invention.
[0036] The invention comprises the following embodiments:
[0037] 1. A process for the production of a PGM-enriched alloy comprising 0 to 60 wt.-%
of iron and 20 to 99 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, the process comprising the steps:
(1) providing a PGM collector alloy comprising 30 to 95 wt.-% of iron, less than 1 wt.-%
of sulfur and 2 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, (2) providing a copper- and sulfur-free material capable of forming a slag-like composition when molten, wherein the molten slag-like composition comprises 40 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 60 wt.-% of silicon dioxide, (3) melting the PGM collector alloy and the material capable of forming a slag-like composition when molten in a weight ratio of 1 : 0.2 to 1 within a converter until a multi-or two-phase system of a lower high-density molten mass comprising the molten PGM
collector alloy and one or more upper low-density molten masses comprising the molten slag-like composition has formed, (4) contacting an oxidizing gas comprising 0 to 80 vol.-% of inert gas and 20 to 100 vol.-% of oxygen with the lower high-density molten mass obtained in step (3) until it has been converted into a lower high-density molten mass of the PGM-enriched alloy, (5) separating an upper low-density molten slag formed in the course of step (4) from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density, (6) letting the molten masses separated from one another cool down and solidify, and (7) collecting the solidified PGM-enriched alloy.
[0038] 2. The process of embodiment 1, wherein the PGM-enriched alloy comprises or consists of 0 to 45 wt.-% of iron and 30 to 99 wt.-% of the one or more PGMs, 0 to 60 wt.-% of nickel, 0 to 5 wt.-% of copper, and 0 to 10 wt.-% of one or more other elements.
[0039] 3. The process of embodiment 1, wherein the PGM-enriched alloy comprises or consists of 0 to 20 wt.-% of iron, 40 to 90 wt.-% of the one or more PGMs, 0 to 60 wt.-%
of nickel, 0 to 5 wt.-% of copper and 0 to 3 wt.-% of the one or more other elements.
[0040] 4. The process of any one of the preceding embodiments, wherein the PGM
collector alloy provided in step (1) comprises 40 to 70 wt.-% of iron, 0 to 20 wt.-% of nickel, less than 1 wt.-% of sulfur and 5 to 15 wt.-% of the one or more PGMs.
[0041] 5. The process of any one of the preceding embodiments, wherein the PGM
collector alloy comprises no more than 4 wt.-% of copper.
[0042] 6. The process of any one of embodiments 1 to 3, wherein the PGM
collector alloy comprises or consists of:
30 to 95 wt.-% of iron, 0 to 20 wt.-% of nickel, 0 to < 1 wt.-% of sulfur, 2 to 15 wt.-% of the one or more PGMs, 0 to 4 wt.-% of copper, and 0 to 30 wt.-% of one or more other elements.
[0043] 7. The process of any one of embodiments 1 to 3, wherein the PGM
collector alloy comprises or consists of:
40 to 70 wt.-% of iron, 0 to 15 wt.-% of nickel, 0 to < 1 wt.-% of sulfur, to 15 wt.-% of the one or more PGMs, 0 to 1 wt.-% of copper, and 0 to 20 wt.-% of one or more other elements.
[0044] 8. The process of any one of the preceding embodiments, wherein the molten slag-like composition comprises or consists of:
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, to 60 wt.-% of silicon dioxide, 0 to 20 wt.-% of iron oxide, 0 to 20 wt.-% of sodium oxide, 0 to 20 wt.-% of boron oxide, and 0 to 2 wt.-% of aluminum oxide.
[0045] 9. The process of any one of embodiments 1 to 7, wherein the molten slag-like composition comprises or consists of:
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, 10 to 60 wt.-% of silicon dioxide, 0 wt.-% of iron oxide, 0 to 10 wt.-% of sodium oxide, 0 to 10 wt.-% of boron oxide, and 0 wt.-% of aluminum oxide.
[0046] 10. The process of any one of the preceding embodiments, wherein the PGM
collector alloy comprises 0 to 4 wt.-% of silicon and wherein the molten slag-like composition comprises 40 to 60 wt.-% of magnesium oxide and/or calcium oxide and 40 to 60 wt.-% of silicon dioxide.
[0047] 11. The process of any one of embodiments 1 to 9, wherein the PGM
collector alloy comprises > 4 to 15 wt.-% of silicon and wherein the molten slag-like composition comprises 60 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 40 wt.-%
of silicon dioxide.
[0048] 12. The process of any one of the preceding embodiments, wherein the PGM
collector alloy and the material capable of forming a slag-like composition when molten are melted in a weight ratio of 1 : 0.2 to 0.8 or 1 : 0.2 to 0.6.
[0049] 13. The process of any one of the preceding embodiments, wherein the temperature of the converter contents is raised to 1200 to 1800 C.
[0050] 14. The process of any one of the preceding embodiments, wherein the contact between the oxidizing gas and the lower high-density molten mass is made by passing or bubbling the gas through the lower high-density molten mass from the bottom of the converter and/or by means of a gas lance the exhaust of which being immersed into the lower high-density molten mass.
[0051] 15. The process of any one of the preceding embodiments, wherein the contact with the oxidizing gas takes 1 to 5 hours.
Examples Example 1 [0052] A premix of 500 kg of a PGM collector alloy comprising 47 wt.-% of iron, 14.1 wt.-% of nickel, 8.1 wt.-% of silicon, 4.6 wt.-% of palladium, 3.2 wt.-% of chromium, 2.5 wt.-% of titanium, 2.2 wt.-% of platinum, 1.8 wt.-% of manganese, 0.6 wt.-% of rhodium and 0.9 wt.-% of copper, 123 kg of calcium oxide, 75 kg of silicon dioxide, 15 kg of sodium carbonate and 15 kg of borax was portionwise introduced into an already 1500 C
hot cylindrical natural gas-heated furnace and further heated to 1700 C.
[0053] After a melting time of 10 hours a two-phase system of a lower high-density molten mass comprising the PGM collector alloy and an upper low-density molten mass comprising a slag-like composition was formed. Oxygen was introduced into the lower high-density molten mass via a ceramic pipe with an oxygen flow of 900 I/min.
After 2.5 hours the oxygen introduction was stopped. The upper low-density molten mass was poured into cast iron slag pots in order to cool down and solidify. The lower high-density molten mass was then poured into graphite molds in order to cool down and solidify.
After solidification and cooling down to ambient temperature both materials were analyzed by XRF.
Examples 2 and 3 [0054] Example 1 was repeated with the difference that the oxygen introduction took 2.75 hours (Example 2) or 3 hours (Example 3).
[0055] The results of the XRF analysis are compiled in Tables 1 and 2. All values are in wt.-%, except the values for the PGM content in the slag which are in wt.-ppm:
Element Example 1 Example 2 Example 3 Fe 29 35 40 Ni 1 1 1 Total PGM 49 47 44 Table 1: Composition of the solidified upper low-density mass (slag) Element Example 1 Example 2 Example 3 Fe 20 18 13 Ni 50 51 51 Table 2: Composition of the solidified lower high-density mass (PGM enriched alloy)
Claims (15)
1. A process for the production of a PGM-enriched alloy comprising 0 to 60 wt.-% of iron and 20 to 99 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, the process comprising the steps:
(1) providing a PGM collector alloy comprising 30 to 95 wt.-% of iron, less than 1 wt.-%
of sulfur and 2 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, (2) providing a copper- and sulfur-free material capable of forming a slag-like composition when molten, wherein the molten slag-like composition comprises 40 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 60 wt.-% of silicon dioxide, (3) melting the PGM collector alloy and the material capable of forming a slag-like composition when molten in a weight ratio of 1 : 0.2 to 1 within a converter until a multi-or two-phase system of a lower high-density molten mass comprising the molten PGM
collector alloy and one or more upper low-density molten masses comprising the molten slag-like composition has formed, (4) contacting an oxidizing gas comprising 0 to 80 vol.-% of inert gas and 20 to 100 vol.-% of oxygen with the lower high-density molten mass obtained in step (3) until it has been converted into a lower high-density molten mass of the PGM-enriched alloy, (5) separating an upper low-density molten slag formed in the course of step (4) from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density, (6) letting the molten masses separated from one another cool down and solidify, and (7) collecting the solidified PGM-enriched alloy.
(1) providing a PGM collector alloy comprising 30 to 95 wt.-% of iron, less than 1 wt.-%
of sulfur and 2 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, (2) providing a copper- and sulfur-free material capable of forming a slag-like composition when molten, wherein the molten slag-like composition comprises 40 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 60 wt.-% of silicon dioxide, (3) melting the PGM collector alloy and the material capable of forming a slag-like composition when molten in a weight ratio of 1 : 0.2 to 1 within a converter until a multi-or two-phase system of a lower high-density molten mass comprising the molten PGM
collector alloy and one or more upper low-density molten masses comprising the molten slag-like composition has formed, (4) contacting an oxidizing gas comprising 0 to 80 vol.-% of inert gas and 20 to 100 vol.-% of oxygen with the lower high-density molten mass obtained in step (3) until it has been converted into a lower high-density molten mass of the PGM-enriched alloy, (5) separating an upper low-density molten slag formed in the course of step (4) from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density, (6) letting the molten masses separated from one another cool down and solidify, and (7) collecting the solidified PGM-enriched alloy.
2. The process of claim 1, wherein the PGM-enriched alloy comprises or consists of 0 to 45 wt.-% of iron and 30 to 99 wt.-% of the one or more PGMs, 0 to 60 wt.-% of nickel, 0 to 5 wt.-% of copper, and 0 to 10 wt.-% of one or more other elements.
3. The process of claim 1, wherein the PGM-enriched alloy comprises or consists of 0 to 20 wt.-% of iron, 40 to 90 wt.-% of the one or more PGMs, 0 to 60 wt.-%
of nickel, 0 to 5 wt.-% of copper and 0 to 3 wt.-% of the one or more other elements.
of nickel, 0 to 5 wt.-% of copper and 0 to 3 wt.-% of the one or more other elements.
4. The process of claim 1, wherein the PGM collector alloy provided in step (1) comprises 40 to 70 wt.-% of iron, 0 to 20 wt.-% of nickel, less than 1 wt.-%
of sulfur and to 15 wt.-% of the one or more PGMs.
of sulfur and to 15 wt.-% of the one or more PGMs.
5. The process of claim 1, wherein the PGM collector alloy comprises no more than 4 wt.-% of copper.
6. The process of claim 1, wherein the PGM collector alloy comprises or consists of:
30 to 95 wt.-% of iron, 0 to 20 wt.-% of nickel, 0 to < 1 wt.-% of sulfur, 2 to 15 wt.-% of the one or more PGMs, 0 to 4 wt.-% of copper, and 0 to 30 wt.-% of one or more other elements.
30 to 95 wt.-% of iron, 0 to 20 wt.-% of nickel, 0 to < 1 wt.-% of sulfur, 2 to 15 wt.-% of the one or more PGMs, 0 to 4 wt.-% of copper, and 0 to 30 wt.-% of one or more other elements.
7. The process of claim 1, wherein the PGM collector alloy comprises or consists of:
40 to 70 wt.-% of iron, 0 to 15 wt.-% of nickel, 0 to < 1 wt.-% of sulfur, 5 to 15 wt.-% of the one or more PGMs, 0 to 1 wt.-% of copper, and 0 to 20 wt.-% of one or more other elements.
40 to 70 wt.-% of iron, 0 to 15 wt.-% of nickel, 0 to < 1 wt.-% of sulfur, 5 to 15 wt.-% of the one or more PGMs, 0 to 1 wt.-% of copper, and 0 to 20 wt.-% of one or more other elements.
8. The process of claim 1, wherein the molten slag-like composition comprises or consists of:
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, to 60 wt.-% of silicon dioxide, 0 to 20 wt.-% of iron oxide, 0 to 20 wt.-% of sodium oxide, 0 to 20 wt.-% of boron oxide, and 0 to 2 wt.-% of aluminum oxide.
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, to 60 wt.-% of silicon dioxide, 0 to 20 wt.-% of iron oxide, 0 to 20 wt.-% of sodium oxide, 0 to 20 wt.-% of boron oxide, and 0 to 2 wt.-% of aluminum oxide.
9. The process of claim 1, wherein the molten slag-like composition comprises or consists of:
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, to 60 wt.-% of silicon dioxide, 0 wt.-% of iron oxide, 0 to 10 wt.-% of sodium oxide, 0 to 10 wt.-% of boron oxide, and 0 wt.-% of aluminum oxide.
40 to 90 wt.-% of magnesium oxide and/or calcium oxide, to 60 wt.-% of silicon dioxide, 0 wt.-% of iron oxide, 0 to 10 wt.-% of sodium oxide, 0 to 10 wt.-% of boron oxide, and 0 wt.-% of aluminum oxide.
10. The process of claim 1, wherein the PGM collector alloy comprises 0 to 4 wt.-%
of silicon and wherein the molten slag-like composition comprises 40 to 60 wt.-% of magnesium oxide and/or calcium oxide and 40 to 60 wt.-% of silicon dioxide.
of silicon and wherein the molten slag-like composition comprises 40 to 60 wt.-% of magnesium oxide and/or calcium oxide and 40 to 60 wt.-% of silicon dioxide.
11. The process of claim 1, wherein the PGM collector alloy comprises > 4 to 15 wt.-% of silicon and wherein the molten slag-like composition comprises 60 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 40 wt.-% of silicon dioxide.
12. The process of claim 1, wherein the PGM collector alloy and the material capable of forming a slag-like composition when molten are melted in a weight ratio of 1 : 0.2 to 0.8 or 1 : 0.2 to 0.6.
13. The process of claim 1, wherein the temperature of the converter contents is raised to 1200 to 1800 °C.
14. The process of claim 1, wherein the contact between the oxidizing gas and the lower high-density molten mass is made by passing or bubbling the gas through the lower high-density molten mass from the bottom of the converter and/or by means of a gas lance the exhaust of which being immersed into the lower high-density molten mass.
15. The process of claim 1, wherein the contact with the oxidizing gas takes 1 to 5 hours.
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US15/355,971 US10323302B2 (en) | 2016-11-18 | 2016-11-18 | Process for the production of a PGM-enriched alloy |
US15/355,971 | 2016-11-18 | ||
PCT/US2017/054370 WO2018093470A1 (en) | 2016-11-18 | 2017-09-29 | Process for the production of a pgm-enriched alloy |
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PL3715483T3 (en) * | 2019-03-26 | 2021-11-22 | Heraeus Deutschland GmbH & Co. KG | Method for producing a pgm collector alloy |
US10472700B1 (en) | 2019-04-29 | 2019-11-12 | Techemet, LP | Converting process with partial pre-oxidation of PGM collector alloy |
US10435767B2 (en) | 2019-04-29 | 2019-10-08 | Techemet, LP | Low-flux converting process for PGM collector alloy |
CN112011696B (en) * | 2020-08-19 | 2021-05-18 | 北京科技大学 | Method for enriching platinum group metal in aluminum-based waste catalyst by pyrogenic process |
CN113528828B (en) * | 2021-07-01 | 2022-06-10 | 昆明贵研新材料科技有限公司 | Enrichment method of waste alumina carrier platinum group metal catalyst |
CN113718109B (en) * | 2021-09-01 | 2022-10-18 | 兰州有色冶金设计研究院有限公司 | Method for determining slag form of electronic waste smelted in molten pool and slag form |
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ZA807646B (en) | 1979-12-31 | 1982-02-24 | Johnson Matthey Co Ltd | Refining of refractory materials |
GB2086941A (en) | 1980-11-05 | 1982-05-19 | Engelhard Corp | Recovery of materials from low concentrations |
JPH028314A (en) * | 1988-09-30 | 1990-01-11 | Hitachi Metals Ltd | Method for refining molten metal |
JP3222894B2 (en) | 1991-04-10 | 2001-10-29 | 田中貴金属工業株式会社 | Platinum group metal recovery method |
AU2008299386B2 (en) * | 2007-09-14 | 2012-01-12 | Barrick Gold Corporation | Process for recovering platinum group metals using reductants |
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